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Fully resolved numerical simulation of reactive mixing in a T-shaped micromixer using parabolized species equations

机译:使用抛物线方程,完全解析T型微混合器中反应混合的数值模拟

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This paper introduces and exploits a hybrid numerical approach for fully resolved numerical simulations of reactive mixing in T-shaped microreactors and thereby enables a computational analysis of how chemical reactions interact with convective and diffusive transport. The approach exploits the fast redirection of the flow inside the mixing channel, resulting in a flow field with positive axial flow component everywhere after a short entry zone. This allows handling the axial flow direction as a pseudo-time variable, so that the evolution of the concentration profile can be computed consecutively on successive cross sections, following the main axial flow direction. With this approach the finest length scales, given by the Batchelor length scale, can be resolved for such a reactive mixing process inside a T-microreactor at stationary flow conditions. This allows for a detailed analysis of the mixing state as well as important characteristics of the reactive mixing process like yield and selectivity. The concrete numerical simulations yield local diffusion times inside the reactor, reveal the influence of the strength of the secondary flow on the progress of the chemical reaction and show how local selectivities result from the species transport.
机译:本文介绍并利用混合数值方法对T型微反应器中反应混合的数值进行完全解析的数值模拟,从而对化学反应如何与对流和扩散传输相互作用进行计算分析。该方法利用了混合通道内流体的快速重定向,从而在短进入区之后的各处都产生了具有正轴向流分量的流场。这允许将轴向流动方向作为伪时间变量来处理,从而可以在跟随主轴向流动方向的连续横截面上连续计算浓度分布的演变。通过这种方法,可以解决由Batchelor长度标尺给出的最细的长度标尺,以便在固定流动条件下在T型微反应器内部进行这种反应混合过程。这可以对混合状态以及反应混合过程的重要特征(如收率和选择性)进行详细分析。具体的数值模拟得出反应器内部的局部扩散时间,揭示了二次流强度对化学反应进程的影响,并表明了物种迁移如何产生局部选择性。

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